Demulsifying and settling tank



Aug. 10, M43 w. ML MQUNT 9 DEMULSIFYING: AND SETTLING: TANK Filed Oct. 14, 1941 4 Sheets-Sheet 1.

Afiga m 1 ,w. M, MUNT 293269334 DEMULSIFYING AND SETTLING TANK Filed Oct. 14, l94l 4 Sheets-Sheet 2 iizlaia 07".

Aug. 1, 3943. w. M. MOUNT 9 59 DEMULSIFYING AND SETTLING TANK Filed Oct. 14, 1941 4 Sheets-Sheet 4 .94 93 95 ,JJAP

Patented Aug. 10, 1943 1 UNITED STATES PATENT OFFICE 7 7 Q 2,326,384; 1 i r Y 'pEMpLsmYrNo ANDsa'r'rLrNo TANK i Walter M. Mount, Tulsa, 0151a. I Application ()ctober 14, 1941, Serial No. 414,961 r 9 Claims. 01. ale-452.5)

The invention relates, to an apparatus fordemulsifying and settling liquids, and has more particular reference to improved apparatus such as shown in my Patent No. 2,156,123 granted April 25, 1939, for removing-excess free Water and sediment from crude oil and similar liquids, and which will also demulsify the oil by breaking down the water-oil emulsions. This application is a continuation-in-part of my application Serial No. 227,385, filed August 29, 1938.

Before crude oil, that is, o il as it is taken from the wells, can be delivered to pipe lines for transportation to distant parts, it is necessary to clarify the oil so that its' content of. water, emulsion and sediment does not exceed approximately one-half of one per cent. Thisrequires,

intensive clarification and demulsification oi the crude oil. For breaking down the ,emulsions,,it is necessary to heat theoil,.which has generally been done in a tank at some distance fromthe well. The water-oil emulsionsmay be considered a mixture of liquids of different specific gravities. The application of heat facilitates the separation of one liquid from the other,;since a liquid of .less specific gravity'will expand at a; greater rate than a liquid of greater specific gravity. As regards water-oil emulsions, the oil is of less specific gravity than the water, and upon the application of heat the oil rises and the Water,

together with the solids and other sediment,

settles to the bottom, e

The most serious objection to apparatus heretofore used for demulsifyingand settling crude oil has been the inefficient use made of the heat added to the oil, and itsr uneven distribution throughout the mass being treated. The present apparatus-is highly efiicient in this respect since all operations, namely, the heating, demulsifying of the oil, and its clarification, are performed within one tank. r

a closed tank having an inlet for the oil at the bottom and an outlet at the top. The inlet discharges the crude oil into a vertical heating chamber, through which the oil flows in an upward direction to be discharged at the top-into clarifying chamber having surrounding relation with said heating chamber. In this clarifyeffected. However, additional treatment is'often required and for this purpose; as illustrated in Figures 1 to 4 hereof or in said Patent 2,156,123, said chamber opens into the tank and;the oil discharged therefrom flows upwardly, andduring this flow further ,demulsification and settling may occur. v

The central location of the heating unit [is advantageous for: uniformly distributing the tion and is concentric "with the heating chamber.-

The heat given off at various heights of the heating unit may be considered as decreasing. up-

wardly, Whereas the amount of heat given off by the oil flowing down in the clarifying cham- A0 The present apparatus essentially consists'of efficient manner.

clarifying chamber concentrically arranged With;

respect to said heating chamber so that the liquid which flows in said clarifying chamber 'is in surroundingrelation with andabsorbs heat from the heatingunit. v

Another object of the invention'is te-provide a device such as described including a heating chamber and a clarifying chamber, wherein the oil or other liquid being treated will have a de creasing velocity from the inlet to the outlet.

In the'present apparatus, the velocity of flow-is a maximum through the heating unit. A reduc tion in the velocity takes place in the clarifying chamber since the effective cross-sectional area of this chamber is greater than that of the heating unit. Theoil from the clarifying cham- 7 her may flow upwardly in thetank, and here again the effective cross-sectional area; is greater than that of the clarifying chamber. 1

- A further object ofthe invention resides in the pro ision of equipment in-the clarifying cham' her which will operate on the counter-flow principle to produce clarification of the liquid. This equipmentpromotes an upward flow of the liquid Withinthe clarifying chamber, and which takes place at a gradually decreasing velocity, whereby i the heavy liquids, sediment ,and foreign matter will havea tendency to flow downwardly or counter thereto towards the discharge outlet.

A further object of the invention resides in the provision of means whereby excess pressures in any part of the apparatusare effectively controlled and'which prevents untreated oil from reaching the outlet of the tank. With these and various other objects in view, the invention may consist of certain novel features of construction and operation as will be more fully. described and particularly pointed out in the'speei-memflrawings-andmims appended therein.

In the drawings, which illustrate an embodiment of the invention, and wherein like reference characters are used to designate like parts-- Figure 1 is a vertical cross sectional showing the improved demulsifying and settling tank of the invention; Y

Figure 2 is a transverse sectional viewtaken substantially on line 2-2 of Figure 1;;and show- 7 ing the concentric relation of the heating chamohamber and tank;

1 Melt is a transverse :sectional view taken isnbmntiflly on line 3- 3 of Figure l;

Figure l isflawertieal cross sectional view show- M a-modified of izlemu'lsi i-ying and settling mik-ccming witliin the invention; and

Figures 5 and 6 are vertical sectional views iho w mg another embodiment f the i-nvent'ion been simplified -"to' include eerily the mhamber and clarifying chamber;

Zln the embodiment 0f the -inven tion disclosed "in Figures 2 and 3, numeral ill indicates the mail mnits, rzan-iel'y, the heating mm and the flurilying are located. The tank H) has a ilep'ing "douse 1 I, sidewalls 2 and top I3. 'The flie heelting urii t, comprising the cylinder -2-2-ex-- tending vertically of the tank'and extendingbe wand. fihetankmfii'rchextensicn iorms the -c-h fer the produc ts of combustion. memuneral 21 indicates the top plate --of the 'heatirrgainit. Extending "vertical-1y within the heating nnit and for -the entire dength "thereof are n pluralityei *fi-re tubes Said tubes err-- tend *throug'h and project "a esher't distance "below 'flaerple tez l Rand ail-w extend through and project a new the topplate 14. productsdr combustion and the burning gases from the' eembus'tion chamber and firebox and fiche-relate temperature, enter the fire 2E and tmvl i'I-hel'eng'th --of the same, to be eventualiy diselrarged from said tubes into tribes is minta'ine'd at a high temperature by the burning flowing therethrough, and the liquid enters the heating chamber at the inlet 25 thereio're has surrounding relation with the iiretu'bes and scion heated to a relatively tempe'ra-tru'e the structure described is verwelfic'ier in heattransfer. -I'heheightof the heaitirrgwmit another factor insuring heating of the eil airether liquid to be treated, to the The highest temperature possible for the amount of heat produced by the burner IT.

The cylindrical wall 22 of the heating unit is provided with a plurality of outlets 2! at the 5 upper end thereof. The heated oil or other liquid from the said heating unit 22 is delivered by the outlets to a clarifying chamber formed 'by the cylindrical walls 28, closed at the top by a member 30. l0 1n this improved form af uemulsiiymg and settankxa-hngle clariiying ehamberis used and'which is disposed in surrounding relation with the heating unit, it being observed that the cylindrical wall 28 is concentric with the wall "1'5 -2=zer=-me heating unit. The clarifying chamber 81 member has an open flaring bottom 3!, and the liquid which flows downwardly through the clari fying rnernber is discharged thereby into the basezof-the tank In. Within the cylindrical Wall 28 is positioned a tray 32 which has a gradual 'slope' toward the periphery the-reo'i and which is *provided wrm adependlng hange'hl. -The-clarifying'meniberiis suitably held in position within the' tank since the top fl ef tank has "connecifron to. cylindrical wall 18 *and also by treason oi =the' connection *between 'the tcp3'8 of --the-dlafiiying member to *the will 22 of the heating cl'raniber. The-tray fl li'kew-ise connects with the wall of the dieaiting -uni't, and i the "depending flange 33 .ispropeidy'Mitioned by members 3! -connecting the lower pentiorn of "the flange with the insiiie mall o'f 'fihe 'ciar'iiying member.

" Below'the periphereil flange $3, the cl'arifying is provided with a'partition 350f inverted '35 em partition termsa base we sludge' baein for t-he clariiying charx-i-ber and is provided w rth one' or more ili dge draw-off-pipes 36 depending from the hm imn tal pipes 31 which "-connectwith flieZbottem of the sludge basin and exterrd outwardly through the wall- 0f 'the tank. Eat-Eli -ei pipes WIis closed at its buteremi b plug 18, which, however, 'isremovable so as willow operator to insert a rod filer the murpoee oi retrieving any deposit wmehmay qu ne up in' the Knee (if "the sludge basin 7 1- "The sludge basin is' 'alsoprovided'with standplpes at extending Wert'ically upward *from "said base and terr-rfin'ating a short distance below the :tmy One war -more stand-pipes nray be provided, equally spacedaround are circumference of' the heating cflia-rrber and relatively close to tlre will 2! thereof. "These pipes form a clear l-iqu'id outlet for the clarifying zone formed by tray "Mend the peripheral dependin'g flange 33 thereof. The is first caused" to -flow downwardly-in the clar'iiyin-g 'cira'nriber "-28 to below the peripheral flange 83; From bare the "liquid will eontinueits "flow "in an upward direction to the clear liquid outlets 40. These outlets "discharge the into the flarin-g 'openyend "3| oi the clarifying member. is shqwn in the drawings,

the-said clari-fying memberatitsopenend'coma withthe interior oft'hetank, and ac- '5 c'erdirrgly the liquid therefrom 'isdischarged into thctank r' Referring again }to "the peripheral flange 33,

it 'wi-llbe pbservedtlraft saidfiange converges inwardly towardfits base to form a peripheral discharge passage with the cylindrical wall of the purifying unit, fand which is of gradually increasing cross-'sectional'area downwardly. On the-other hand, the-zone formedby the tray and the' depending flange increases in cross-sectional 15 areain-adirecficnupward y. Asa result 'of'th'i's central discharge passage.

pending flange, times open and the flow of liquid is gradually de- .said tray and depending flange.

2,326,384 desigmthevelocity of flow of the liquids and solids tends to decrease both in the discharge passageway as well as in the clarifying zone. The result obtained is a higher clarifying capacity for a given volume tank.

Since the object is to gradually decrease the the clear liquid'outlet, it is obvious that a peripheral discharge passage is providedinstead of a The increase in cross-sectional area of the discharge passage in a downward direction, in addition to the 'decrease the velocity of the liquid flowing through said passage, effectively eliminatesthe settling or collection of the solids on thede- Therefore, the passage is at all creasing, and which continues as the liquid flows upwardly within the clarifying zone formed-by As a result of this slow movement of the liquid, the heavy parholes are precipitated, and even the finer particles are filtered from the liquid so that only the clarified liquid reaches the outlet formed by the stand-pipes 40. I n r The action of the clarifying tray in clarifying the liquid as; above described, is also highly efiicient for breaking down emulsions such as the water-oil emulsions in the crude oil. As described, this breaking down of the emulsions requires the application of heat to the liquidsince .heat facilitates separation of one liquid from the other. ,The oil is of less specific gravity than water, and thereforeithe oil will rise and flow into the clarifying zone. During this movement of the oil, intensive demulsification thereof takes place since the tendency of the water is to settle. The settlingout of the water is further aided by thefine particles in suspension in'the liquid at the entrance of the clarifying zone. There is a tendency for these fine particles toform in layers segregated according to size and density, and theselayerslform an excellent filter for the risingdispersion medium. The settling of the water, solids and other sludge is towards the sludge basin 35, and the same is removed by oneor more sludge draw-ofis 36.

I .A material reduction in flow of the clear liquid downwardly from the end of the stand-pipes 4D is obtained due to the fact that the quantity of liquid has been reduced by the removal of the water, sludge or other foreign particles therefrom. This flow of the clear liquid further is graduall reduced as a result of the flaring open end of the clarifying unit. From the clarifying unit, the clear liquid is discharged into the tank, the efiective cross-sectional area of which is greater than the efiective cross-sectional area of the said clarifying unit. .This is in accordance with the invention, whichcontemplates a reduction in velooity of flow from the heating unit to the clear liquid outlet .41 located in the upper portion of thegtank. The flow of the liquid within the tank Ill therefore is in an upward direction, and this direction of flow, as previously described with respect to the clarifying zone, promotes settling of the' water and-sediment tothebottom of the tank.

The water and sludge draw-off 52 is ocated in the bottom portion of the tank ill, the same being provided with a valve indicated by numeral having regulating means 44. Above the drawofi lf-2 the tank is provided with a flanged connection within which is located a ball-float 58. Said float is secured to shaftll journalled byth connection 45, andiOne end of which extends through-the packing gland.48 The out-- wardly extendingend of the, shaft 41 is connected by the rod 5llwith the regulating-means 44 of the valve-43.

During operation of the demulsifying tank, the waterlevel will be maintained substantially constantby the float 46 since movement of thefloat upwardly, wh ich takes place'when the water level rises, willactuate valve 43 to open the draw-off, thereby lowering the water level within the tank; The travel of the clear liquid, such as oil discharged from the stand-pipes, will take place through water, and likewise the flow upwardly between the ,tankwalls and the flaring bottom-3| of the clarifying chamber will take place through I thebody'of water maintainedwithin-the bottom portion of thetank. gTh e liquids,-however, will .be at a relatively high temperature, and this flow, together with the high temperature, promotes I the breaking down of Tany water andoil emu1- sions in the crude oil.

In order to equalize the pressure within the tank, clarifying chamber and within the clarifying, zone, the invention, provides gasrelief vents in the'form of upwardlyidirected pipes'fil and 52. Pipe 5L extends upwardly from the tray 32 and serves to. relieve excessive gas pressures which build up under. the tray. In the event some liquid may be located in advance of the. gas, the

said liquid will be discharged from the top of pipe 51 and will ,be-returned to theclarifying chamber.. ,Pipe 5;2 serves tovent the top portion of thetank, andhere againthe open end. of the vent will discharge into the clarifying chamber.

may beinadvertentlyncarried .by-the excessive gas pressure will be returned to the clarifying chamber for further clarification and demulsification, Theconnection 53 encloses the upper end of pipes 5| and.-2, and is provided with which the gas is withdrawn The central location of heating unit withinthe tank 10 isadvantageous for" distributing the heat throughout the mass of oil in the tank.

Theliqui'd discharged fromope ning s- 21 is at a relatively high temperature, and as this; high;

temperature liquid flows downwardly, hefat is given-01f thereby to the oil in the-upper portion of the tank; 1 However, heat is given off to the liquid as it-flowsdownwardly in the-clarifying chamber, since the chamber is'con'centricwith and in surrounding'relation with the heating unit. 7

y I The present apparatus has -been designed to maintain a I comparatively even temperature throughout the mass of liquid in the tank. This is largely responsible for the high efliciencyof the appara-tus in breaking. down the emulsions and settling the foreign particles frorrithe liquid.

'Alloperations that is,,. the heating, clarifying and dem'ulsifying'of. the liquid, are performed within one container}. andnaccordingly less. heat is required to secure the desiredresults than hashere :tofore been -p0ssible. The -invention contem platesusing thegaspi oducedas a result ofith'e heating of the oil for operating-the burner 93,, andsincejoomparatively,very litt e fuel is re-'- quired-tooperate the present apparatusibeoause of its high eificiency, it is believed that-the gas withdrawn fromthe gas: outlet 54 will-be suf ,ficient for operating the said burner. V I v The modified form of tank shown'iniFigureA may be operated ata highwater level or at-a base H.

low water level? depending 'onfthe-behavior of 1 the crude oil 'or otherliquid p'asing the *tankfIn the structure of Figure l'thefloat-fl controls the water le ve'l'arid which may be described as a relatively high level, requiring the clarified liquid discharged from the standpipes 10 to passdownwardly'through 'a body of'salt water, in the case of crude oil'demulsification', and then upwardly also through a body of salt water surrounding theope'n flaring bottom of the clarifying chamber. Certain types of crude oil are benefited by thistravel through the high temperature saltwater lriftha'trin'y emulsions are "caused to" settle out. However", other typesof crude oil react adversely andt'end to combine with thesalt water during travel therethrough, thus increasing their content of water-oil emul- :sions'f For such -oils the modified device of Figure 4 has been primarily designed since in this embodiment of the invention the tank can be Op.. eratedat a low water leveli a The changes reside in providing "the interior of the clarifying: chamber with a zn'einber' fifl forming a sludge basin with respectto theitr'ay 32 and depending flangefn and Which.'sludge basin is substantially open 'at itslower end since member 89 is spaced from the heating chamber 22. Through thi annular opening, indicated by numeral 5!, the salt water, sludge and other liquids settling out in 'the clarifying Zone will be discharged. into a chamberjtl formedby the member 50 and a partition 53. The saltwater, sludge and other liquids entering said chamber can escape therefrom only bypassing through an outlet provided by the flanged connection 64. Pipe 65 forms said outlet and is @provided with the float controlled valve 66. 'Thej'float 61 is located within chamber 62 or more properly within 'the' flanged connection 64 leading from said chamber and is journalled by shaftJ68 extending out from one side of 'saidgconnection. The linkage 68 operatively connects said shaft and thus the float with the valve'fifi so thatthe water and sludge in the chamber iris maintained at 'a fairlyuniform levels; From valvejfifi pipes and H conduct the liquid anddischargethesame into the atjits bottom relatively close to the V Said tank isprovidedfjwith*a ,second flanged connection 1-2' which is on approximately the jrloat controlled valve '66; whereupon the same will be deposited in theflower end of the-tank H. Here the liquid level is maintained at a'relatively uniform height by the float 13 and'whichheight is approximately that of said float when horizontal,'as shown in Figure 4. With this "low water level the 'oilfrom the standpi'pe 40 will be dischargedqinto "the'lower flaring end 3| of the clarifying chamber. As the water level isconsiderably'below the said chamber this clarified oil will not come in contact with the saltwater but will flow around the bottom end of said chamber andupwardly through the tank Without into association with any-"salt water. a j

When it is desired to operate thetank on a high water' level the plug 80. is removed from outlet 18 and' thus the liquidfrom chamber 62 linkage l5. Said linkage aotuatesthe .valve, .116 a located in the outlet pipe- H for the tank. The

valve 1 5 is therefore also: float controlled and the water and s'ludge'from the tank is drawn o'i'f 'at a rate to maintain alow water level within saidztan'k. if V I Before describing the operation of the above structure it must-be f-mexitionedthat the 'cham ber 62 hasan outlet 'in theforrn of pipe 18 which leads directly from said chamber into the lower end .of tank l0, terminating relatively close to 'the bottom H.- I This: outlet from chamberv 62 therefore by-passes the float controlled valve $6.5. I'Iowewar, when the tanIi is'being operated on the low water "level theou'tl'et "I8 is closed by the I cap 8-). It will therefore 'beseen that any solid, wa-terpsludge andother'liquid settlingout-of the oil and which. is caught by the sludge basin will be immediately discharged throughthe annular opening 6! into chamber "62. This chamber is closed offfromtheoil sand with outlet 18 closed by plug the liquid. :must drain through the will by-pass valve 65 and will be discharged directly to the bottom of the tank. The upper "ball float 6-1 is then operatively connected in a manner as suggested in Figural with the float controlled valve 16." The water will build up within the tank and-will eventually. reach a level within the tank equal t o that of the ball float 61. It will be clearly understood, or .course,'that the water level in the tank will equalize with that "within chamberfil since the partsare connected through pipe 78. When the apparatus is operated in "this manner a high water level exists and "the'clarified oil discharging fromstandpipe "40 will pass downwardly through this wate and removable cover 93* for closing. the openingin saiddomed top and which'provides a vent pipe 94 for gases to prevent their accumulation within the member. A drain 95is located adjacent the domed bottom 9|. The cylindrical member 'is suitablysupported by structure 96' and the channel legs 9'! also support on the same foundation the cylindrical jacket 88 surrounding .the fire tube Hill. The exteriorfjacket forms with said fire tube anannular space for initially heating Ithecrude oil or other liquid in advance of delivering the same to the heating chamber.

' The jacket 98 is secured to the cylindrical member at the basethereof bymcans of flanges ifllt'and which seal said end of the jacket with respect to the fire tube. The outer end of the Jacket is also closed by wall 102 and the interior space thus formed is provided'with afvent Hi3 andwith'an-inlet N34 for the crude oil. The axtally. extending fire tube run is 'pronce'awan a burner I "5 connecting with the inlet pipe 10.5 for the gas, having anair adjustment .at .I The burner provides the; main heating unit for heating the liquid to be treated, the liquid entering the jacket byinlet I94. and after flowing the length of'the same the liquid. which has now been initially heated, will leave the annular'space by the outlet I08. Said outlet, as best shown in Figure 6, connects with pipe 39 which at I I0 enters the'cylindrical member at the lower end thereof. This lower end of the member forms an means of the auxiliary bottom III. The heating chamber I I2, which extends vertically within'the cylindrical member, connects with the auxiliary bottom III to close off this end of the chamber and the same also connects with the fire tube I00. The pipes H3 for the liquid extend withinthe heating chamber and project from the respective ends of the same. ,At the base the pipes extend through the auxiliary bottom III and therefore into thechamber for the liquid located below this auxiliary bottom wall. By projecting above the upper end of the heating chamber thepipes extend into and communicate with the clarifying lects the foreign matter and sludge in Figuresl- III' the same manner as the sludge basin cola and 4. Theclari-fying means including tray chamber formed by the cylindrical member 90. g

The gases and products of combustion are con ducted from the heating chamber by the flue II4 which extends through the domed top 92 of the member. 7 v

This form of the apparatus is similar to that shown in Figures 1 and 41in the provision of clarifying means in surrounding relation with the heating unit. Said clarifying means includes the tray I I5 which encircles the heating chamber I I2 and has a gradual slope toward the periphery thereof. At said periphery the tray is provided with a depending flange IIB which is directed inwardly to a slight extent in a downward direction so as to form with the walls of the cylin-' drical member a peripheral passage of gradually increasing cross sectionalarea in a direction downwardly. The depending flange is concentric with the heating chamber and is suitably supported from the cylindrical member by the supports Ill. The vent pipe II8 connects with the tray H5 and extends upwardly within the clarifying chamber to communicate with the inverted cup i which forms an oil trap. The vent pipe functions to vent the gases from under the tray by conducting them to the upper part of the clarifying chamber and therefore the pressure within the clarifying zone formed by said tray and depending. flange is equalized with that in the clarifying chamber. T One or more outlet pipes I2I are located between the depending' flange and the heating chamberc The entrance and flange H6 forma clarifying zone in surrounding relation 'withthe heating chamber through which the liquid'is required to now inan upward direction. During this upward flow de-- niulsification of the liquid is completedina manner similar to that heretofore described'withrespect to Figures 1 and 4 and the water and other foreign matter caused to settle out is deposited by gravity in the base of the tank formed. by the auxiliary bottonrI I I.' The tank is drainedperiodically by the sludge draw-01f I223; The clear liquid which rises to the top of the clarifying zone overflows into the outlet pipe IN and the clear liquid'is drawn off from said clarifying chamber by means of said outlet pipe. f

The invention is'not to be limited to or by de-' tails of construction of the "particular embodiment thereof illustrated by the drawings, as various other forms of the device will of course be apparent to those skilled in the art without departing from the spirit of the invention or the scope of the claims. I

What is claimedis: I l. III-apparatus for demulsifying and settling liquids, a cylindrical member, a top and bottom for said member forming therewith a clarifying chamber, said member having an outlet for withdrawing foreign' matter and sludge from said chamber, a heating chamber extending through the said bottom and axially within the clarifying chamber; a'raw liquid inlet connecting withthe heating chamber at the basethereof and an' outlet in its upper end for discharging, heated liquid into the upper part of the clarifying chamber, atray within the clarifying chamber'and encircling the heating chamber below the outlet, a peripheral flange depending from said tray and terminatingabove said bottom,.said' dependto said pipes formedby the, open end thereof is positioned directly below the tray II5 and said pipes extend to the bottom portion of the cyline drical member, at which point they pass -o.ut irough the wall thereof. The outlet pipe in passing through the wall of the member is effectively sealed by the parts I22. r

In the operation of the form of the invention shown in Figures 5 and 6 the crude oil-or-other liquid to be treated upon enteringthe space provided by jacket 98 is initially heated as the same is caused to flow around the fire tube I00; The heated liquidis then admitted to the base of the cylindrical member at] I0 and from this bottom chamber the liquid flows upwardly through the tubes 3 to be discharged into the clarifying chamber at a point above the tray II 5. Considerable heat is imparted to the liquid during its chamber the liquid will initially flow throughthe peripheral passage, and since the same is in a downward direction the heavy particles, foreign matter and sludge in the liquid are caused to settle out by gravity and deposited'on the bottom ing flange havingspaced relation with the cylindrical member thus providing an annular pas sage through which the liquid flows in a downward direction, said tray and flange forming an inner clarifying zone in surroundingrelation with the heating chamber and within which zone the liquid flows upwardly, and ano utlet for clear liquid in the clarifyingv zone directly below the tray. z v

2. In apparatus. fordeinulsif-ying and settling liquids, a cylindrical'member, a top and bottom forsaid memberformingtherewith a clarifying up-flow within the heating chamber and the i chamber, said member having an outlet for withdrawing foreign matter and sludge from said chamber, a heating chamber extending through the said bottom andaxially within the clarifying chamber, a raw liquid inlet connecting with the heating chamber at the base thereof and an outlet in its upper end for discharging heated liquid into the upper part ofthe clarifying chamber; atray within the clarifying chamber and encircling :the heating chamber below; the outlet, a peripheral flange depending from said trayand terminating above said bottom, said depending flange having spaced relation with the cylindrical member thus providing an annular passage'through which the liquid flows in a downward direction, said tray and flange forming an inner' clarifying zone in' surrounding relation with the heating chamber and within whichzone the liquid flows upwardly, an outlet for clear-1 liquid in the clarifying zone directly b elow the tray,-

and means for venting the gases from within the ari y n Zane, t r the pp r end of. he inr ca i nemh ri 3.. na de uls. s-c amber. e tendin -v rt ally Within the-tank: a d having ai n e for rewi ida e base-9 he i amb r a. ar.i i n m m e W t th nk diseased in qn e riiq. q qnvfih th he tinachambe said? membe h vin a upg tant r. dsedten an L mma itmn term, asi a i- 'ns ehambenfih h in hamb r iar-J s n .qii le t 412, end. e i q e eine heatedliquid nterns: rupee? P 7 .Q weet 9 amber where y th iq ow upwardly, nfi he in ch ber a d. d wn in he lari in chambe t9; be d sc a d t h ank. win em qttem 9? the e ii mg. n e rnber, 'rne ans vvithiri the clarifying chamber in encircling relation with ith e heating chamber iqr separating sludge and other foreign matter from liquid. reversing the direction of flow to, establisl'i la n intermediate zone of upward flow,

an outletim cl'earlqui'd in the upper portion of the tankjan'd a'sl 'g' fbi tifei in'the base of the tank, 7

In a ti'en'i'ui'siiyi'ii'g ands'ettli'ng tank, aheat: ing chamber extending vertically within the tank and having an inlet forraw lidui'd at the base oji'ith lciian'iber;'ii ii irying' chamber within the "dispbsei "in? oncentric, relation with the ""charnb'erfand' having a closed ton and outletifi'n discharging heated liqui diippr part o'jthe clarifying 'cham e' s in the clarifying chamber v7 gfzdiiei aving surrounding thejheating chamber and within outlet, for the, clearli quid ih 'the clarifying zone E i EQfiQFQQWW h'art and d har in within l the, open bottom end of the clarifyin chaniber; a d ravv-ofi for the cl ear liquid in'the upper portioncf'the' tank; and a sludge cutlet:

in the base of the ,tanlg.

5]. Ina den ulsif ying and settling tank,xa heating chamber extending vertically within the tank nsani isttii a tank, heatquidfic'ws upwardly, ainaitititih-in' tli" c larifyin g charnber providing a sludge basin iri'esp'acedrelation below the clarifying zone, an i ill and havirig an inlet for'law liquid at the base of thech'amber, a clarifying chamber within the tank disposed in concentric relation with the heating chamber and having a closed top I andan open bottom, the heating chamber having-an outlet in its upper end -fordis'- charging heated liquid into the upper part of the clarifying-chamber, clarifying means-in the clarif'yin'g chamber including a tray encircling the heating-chamber below the outlet a peripheraldependingflange provided by said tray,

' chamber providing asludge basin in spaced relationbelow the clarifying zone, ancutlet-for the clear ,liquidin the clarijying zone extending through the partition and discharging within the fif i btt ml id hir ng l ify g. am r ,.a

7 and outle for discharging t r .7 W, 30 anppenbottom, the heating chamber havingan aaaaasa:

' rawr fiio v he cle r. iqnid nthe upper p r io he-tank and:.,meens-i fer-ventin he: ases rom under; h trav: 9 e ualize; h pre ure, within the ciarify nsrzqne andswit i he: an; ing chem, 9 i h, the pr ssur n; the np pprtiQn-e thetanh,

enria aiue' fiemulsitxins n e t n i u riealzhnhhafiee an out e for the; ankiga P es? ha n a. dep ndin flan e eated-W t in a d. ,qharhber andforming means. for clarifying the liq id b foreign liquids sludge and other part lls r rem, a1sludge'basinrprovided below shd clarifying rneans, means forming a compartment belo vv'the' sludge basinand' within said clariiying, chamber for receiving the separatediliduids' sludge: and other' particles from the sludge .bas n'; dlraifi for said compartment d scharging? triefthtt'difLpciriiori of the tank, gh s' dxcoinpajrtment liqu d/from the clarifying rnean's' into the .open' end if Said chamber. 7. In apparatus for; d iinisiiyirf and settling liquids, a cylin'di ical tarifl t', a gel ifying chamber injthe tank havingjar'i' inlet f aw liquid at its p end; id l i iifig h.a in an open boptoiriwn eby iidiiiai fiows through the saii e adownwar chi and isd sciiiiiged m a-pjei iphera dependingflange loi etd withinsaid "c amber and forming a clarifying: Zone for the" liquid for separating foreign'liquids, sludge and other particles therefrom, as'nrdgeua rovided below" said clarifying zone, iiie'a ""fojrnnrig a cdinpartrne'iit andifiithih j'said clarifying chamber; iorfreceivirig the separated liquids, sludge an dhtherparticles i the sludge basin, a drain for-said con'ifiart t discharging into the lower endpf the" tahkpfioat controlled means;

,fo'r-said drei'nfoui etsiiiassiii ithrcueh the sludge basin and saidfcc'irr'ipartr'nent for withdrawing the clear-'liquidffrorn the clarifying 'zone and discharging the sanie inte theiopen bottom end of said Chalh blfl'; a clearliquidf dtlet in the upper portion of the tanlc' of the winner-th other-particle s-; 8': In apparatus" for der'niilsi-fyingarid settling liquids, 'a cylind'rieal tai-ilg having'an outlet for nilan outlet in the base iseparated liquids, sludge or clarified liquid, an inlet chamber-brine liquid disposedNerticrllybf-ththrik and through which the liquidlfl'ows in -aii upward direction; a-clarify eign liquid; sludge :and i other-particles from the liquid flowing .therethrough, a sludge basin provided, by said clarifying chamber belowsaid means for collecting the separated liquids, sludge and jother particles, ;a partition "in the clarifying chamber forming a c'ompartmen't b'elow the sludge basin ,and in surroundingrelatiori -.with the inlet chamber ,for receivingthe liquids and sludgefrom the sllld e :basin, a drain for-'said compartnient hav n QQBI-Ection; with saidtank atthe lower end thereof whereby said separated liquids and sludge are discharged into the lower portion of said tank, a drain for said tank, and means for conducting the clear liquid from said clarifying means and for discharging the same into the tank. H e

9. A demulsifying and settling tank for liquids including a vertically extending inlet cylinder with the inlet cylinder at its upper end, saidsec- 7 0nd mentioned cylinder at its lower end opening into the tank whereby theliquid flows upwardly in the inlet cylinder and downwardly in the sec J and mentioned cylinder to be discharged into the tank, means 'for clarifying the liquid withinthe second mentioned cylinder havingnsurrounding relationwith the inlet cylinder, said means reversing the direction of flow to decrease the rate of flow of the liquid through said means,,where-i by foreign liquids, solids and other matter'are caused to separate out by gravity, an outlet "in the base of the tank for said foreign liquids, solids and other matter, and an outlet in the upper portion of the tank for the c'larifiedliq uid,

WALTER M. MOUNT. 

